
Process Risk Assessment: SIL Methodology and Assessment Techniques and tools
$5500.00
🎯 Process Risk Assessment: SIL Methodology & Assessment Techniques - 5-Day Course
Duration: 5 Days | 5 Hours Daily | 25 Total Hours
Level: Intermediate to Advanced
🎯 Course Overview
Intensive training on Safety Integrity Level (SIL) determination, LOPA, HAZOP, and risk assessment tools per IEC 61508/61511 and ISA 84 standards.
Target Audience: Process safety engineers, SIS engineers, instrumentation engineers, HAZOP leaders, risk assessment specialists
Prerequisites: Engineering degree, basic process safety knowledge, understanding of P&IDs
📅 DAY 1: Risk Assessment Fundamentals & HAZOP
Learning Objectives: Master risk assessment principles and conduct HAZOP studies
Modules:
1.1 Risk Assessment Principles
Risk definitions: hazard, likelihood, consequence, ALARP
Qualitative vs. quantitative methods
Risk matrices and acceptance criteria
F-N curves and risk tolerance
1.2 HAZOP Methodology
HAZOP process and team roles
Guidewords: No, More, Less, Reverse, As Well As, Part Of, Other Than
P&ID review and node selection
Deviations, causes, consequences, safeguards
Action tracking and documentation
Workshop: HAZOP facilitation techniques
1.3 HAZOP Practical Exercise
Team-based HAZOP on separator/reactor system
Complete study on provided P&ID
Deviation scenarios and safeguard identification
Hands-On: 2-hour HAZOP study exercise
1.4 Consequence Analysis
Fire modeling: pool fire, jet fire, flash fire, BLEVE
Explosion modeling: VCE, confined explosion
Toxic dispersion: Gaussian plume, dense gas
Impact zones and safety distances
Demo: PHAST/ALOHA software
Deliverable: HAZOP study report
📅 DAY 2: Layer of Protection Analysis (LOPA)
Learning Objectives: Master LOPA methodology, identify IPLs, and determine SIL requirements
Modules:
2.1 LOPA Fundamentals
LOPA methodology per CCPS guidelines
Relationship to HAZOP and IEC 61511
Team composition and documentation
2.2 Initiating Events
Initiating event identification and frequency
Generic data sources: CCPS, PDS, OREDA, API 581
Common frequencies:
Pump failure: 1×10⁻¹/yr
Pipe rupture: 1×10⁻⁴/m-yr
Operator error: 1×10⁻¹ to 1×10⁻²/demand
Control valve failure: 1×10⁻¹/yr
Exercise: Initiating event frequency determination
2.3 Independent Protection Layers (IPLs)
IPL criteria: effectiveness, independence, auditability
IPL categories with typical PFD:
Process design: 10x (PFD 0.1)
BPCS: 10x (PFD 0.1) - specific criteria
Critical alarms + operator: 10x (PFD 0.1)
SIF: SIL 1-4 (PFD 0.1 to 0.0001)
Relief devices: 10x-100x (PFD 0.1-0.01)
F&G + mitigation: 10x (PFD 0.1)
IPL independence requirements
Workshop: IPL identification exercise
2.4 LOPA Calculations
Risk tolerance criteria
MEL = Initiating Event × ∏(PFD of IPLs)
Required RRF = Initiating Freq / Tolerable Freq
SIL determination from required PFD
Hands-On Lab: 10+ LOPA scenarios with calculations
2.5 Advanced LOPA
Multiple initiating events
Enabling events and conditional modifiers
Common cause failures
Demand rate effects
Case Study: Complex LOPA scenarios
2.6 LOPA Documentation
Worksheet structure and templates
IPL justification
SIL assignment documentation
Exercise: Complete LOPA documentation
Deliverable: LOPA study with SIL requirements
📅 DAY 3: SIL Determination & Verification
Learning Objectives: Master SIL selection methods and perform detailed verification calculations
Modules:
3.1 SIL Overview
IEC 61508, IEC 61511, ISA 84 standards
SIL levels and PFD ranges:
SIL 1: 0.1 to 0.01 (RRF 10-100)
SIL 2: 0.01 to 0.001 (RRF 100-1,000)
SIL 3: 0.001 to 0.0001 (RRF 1,000-10,000)
Low demand vs. high demand mode
3.2 SIL Selection Methods
Risk Graph method (IEC 61511)
Risk Matrix method
LOPA method (Day 2)
Quantitative Risk Assessment (QRA)
Workshop: SIL determination using multiple methods
3.3 Reliability Engineering
Failure rate (λ), MTTF, MTTR, PFD
Failure modes: DD, DU, SD, SU
Safe Failure Fraction (SFF)
Diagnostic Coverage (DC)
Proof test coverage (PTC)
Common cause (β factor): 2%-10%
3.4 SIL Verification Calculations
Single channel (1oo1):
PFDavg = (λDU × TI) / 2
Redundant architectures:
1oo2: PFDavg ≈ β×(λDU×TI)/2 + (λDU×TI)²/3
2oo3: PFDavg ≈ 3×β×(λDU×TI)²/2 + (λDU×TI)³
2oo2, 1oo3, 2oo4, MooN configurations
Typical failure rates:
Pressure transmitter: λDU = 0.5-1.0×10⁻⁶/hr
Temperature transmitter: λDU = 0.3-0.8×10⁻⁶/hr
Logic solver: λDU = 5-20×10⁻⁶/hr
Shutdown valve: λDU = 1-5×10⁻⁶/hr
Hands-On Lab: SIL verification for multiple architectures (2 hours)
3.5 Reliability Data Sources
OREDA, PDS, SERH, IEEE 500
Manufacturer data vs. generic data
Environmental adjustment factors
Exercise: Data source selection
3.6 Proof Testing
Proof test intervals and coverage
Effect of PTC on PFDavg
Partial stroke testing
Interval optimization
Workshop: Test interval determination
3.7 SIL Verification Software
exSILentia, SILcalc, SINTEF tools
Reliability block diagrams
Fault tree analysis for SIS
Hands-On: Software exercises
Deliverable: SIL verification calculations
📅 DAY 4: Advanced Risk Assessment Tools
Learning Objectives: Master FTA, ETA, Bowtie, and QRA methodologies
Modules:
4.1 Fault Tree Analysis (FTA)
FTA methodology and symbols
AND/OR gates and Boolean algebra
Top event probability calculations:
AND: P(Top) = P(A) × P(B)
OR: P(Top) ≈ P(A) + P(B) (rare events)
Minimal cut sets
Hands-On: Develop FTA for process scenario
4.2 Event Tree Analysis (ETA)
Initiating events and pivotal events
Success/failure branches
Sequence frequency calculations
Integration with FTA
Case Study: Fire scenario ETA
4.3 Bowtie Methodology
Central hazard identification
Preventive barriers (threats to hazard)
Mitigative barriers (hazard to consequences)
Degradation factors
Software tools: BowTieXP
Workshop: Develop Bowtie diagram
4.4 Quantitative Risk Assessment (QRA)
QRA framework and methodology
Frequency assessment techniques
Consequence modeling integration
Risk metrics: IRPA, PLL, FAR, F-N curves
Risk acceptance criteria
Case Study: Offshore/chemical plant QRA
4.5 Human Reliability Analysis (HRA)
Human error types and probability (HEP)
Methods: THERP, HEART, CREAM
Performance Shaping Factors
Typical HEP values: 1×10⁻³ to 1×10⁻¹
Operator action credit in LOPA
Exercise: HRA calculations
4.6 Software Tools
PHAST: consequence modeling
ALOHA: toxic dispersion
Fault Tree+ / RiskSpectrum: FTA/ETA
BowTieXP: barrier management
exSILentia: SIL verification
DNV Safeti: QRA
Hands-On: Software demonstrations
Deliverable: FTA/ETA report, Bowtie diagram
📅 DAY 5: Applications & Capstone Project
Learning Objectives: Apply techniques to real scenarios and complete integrated project
Modules:
5.1 Safety Requirements Specification (SRS)
SRS content per IEC 61511:
SIF description and safe state
SIL assignment with justification
Response time and proof test interval
Functional and integrity requirements
Bypass and reset requirements
Templates and best practices
Workshop: Develop SRS for 2 SIFs
5.2 Application-Specific Risk Assessment
HIPPS: SIL 3 requirements, <2 sec response
Burner Management Systems: SIL 2-3, NFPA 85
ESD Systems: Multiple inputs, depressurization
Tank Overfill: SIL 2, time-to-overflow
Case Studies: Each application
5.3 Documentation & Lifecycle Integration
Study report structure
HAZOP, LOPA, SIL reports
Action tracking and closeout
Risk studies in project phases:
Conceptual: HAZID
FEED: Preliminary HAZOP, LOPA
Detailed: Final HAZOP, SIL verification, SRS
Operations: Revalidation (5 years)
5.4 Quality & Peer Review
Competency requirements
Common pitfalls to avoid:
Missing safeguards
Incorrect IPL credits
Over-crediting operators
Ignoring common cause
Independent verification
Functional Safety Assessment (FSA)
Workshop: Peer review exercise
5.5 Capstone Project
Integrated Risk Assessment:
Teams develop complete study for assigned unit (distillation, reactor, separator, tank farm):
Deliverables:
HAZOP: 2-3 nodes with deviations, safeguards, rankings
LOPA: 5+ scenarios with IPLs and SIL determination
SIL Verification: 3 SIFs with architecture and calculations
Additional Analysis: FTA, ETA, or Bowtie
SRS: Complete specifications for 2 SIFs
Report: Executive summary, methodology, findings, recommendations
Presentation: 25 minutes + Q&A
5.6 Best Practices & Lessons Learned
Case studies of failures
Common errors and solutions
Industry incidents analysis
Continuous improvement
5.7 Professional Development
Certifications: TÜV FSE, ISA CAP-S, CFSP, HAZOP Leader
Advanced topics: Cybersecurity (IEC 62443), AI in risk assessment
Resources and communities
Course evaluation
Deliverable: Complete risk assessment project
🛠️ Standards & Software
Standards: IEC 61508, 61511 | ISA 84 | CCPS LOPA | API RP 754, 520, 521 | NORSOK Z-013 | ISO 31000
Software (Hands-On): exSILentia | PHAST | ALOHA | BowTieXP | Fault Tree+ | SILcalc
Databases: OREDA | PDS | SERH | IEEE 500 | OGP Risk Data
Excel Templates: LOPA worksheets | SIL calculators | Risk matrices | Reliability data
📚 Course Materials
Technical manual (450+ pages)
Standards excerpts (IEC 61511, ISA 84)
25+ case studies
Excel calculation toolbox
Software user guides
LOPA/HAZOP templates
SRS template library
Reliability data compilation
Certificate (40 PDH / 4.0 CEU)
90-day technical support
🎓 Learning Outcomes
✅ Facilitate HAZOP studies per IEC 61511
✅ Conduct LOPA and identify IPLs
✅ Determine SIL using multiple methods
✅ Perform SIL verification for all architectures
✅ Apply reliability data (OREDA, PDS)
✅ Develop Safety Requirements Specifications
✅ Conduct FTA, ETA, and Bowtie analysis
✅ Perform QRA with consequence modeling
✅ Use industry software (exSILentia, PHAST)
✅ Integrate risk assessment in project lifecycle
📞 Enrollment
Delivery: In-Person | Virtual Live | On-Site Corporate
Locations: Houston | Aberdeen | Singapore | Dubai | Calgary
Class Size: Maximum 18 participants
Discounts: 15% group (3+), 10% early bird (45+ days)
🔍 Keywords
SIL determination | Safety Integrity Level | LOPA training | HAZOP course | IEC 61511 | ISA 84 | Process risk assessment | SIL verification | Functional safety | Risk assessment tools | FTA ETA | Bowtie methodology | QRA | exSILentia training | PHAST software | SRS | OREDA PDS | IPL analysis | Process safety | Oil gas safety
⭐ Why This Course?
✔️ 60% hands-on calculations & software
✔️ Training on exSILentia, PHAST, BowTieXP
✔️ Real reliability data (OREDA, PDS)
✔️ Excel toolbox included
✔️ Expert instructors (20+ years)
✔️ Global recognition (Shell, BP, Chevron)
✔️ 40 PDH / 4.0 CEU


